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CN101575321B - Production method of trimetazidine and its hydrochloride - Google Patents

Production method of trimetazidine and its hydrochloride Download PDF

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CN101575321B
CN101575321B CN2009100995184A CN200910099518A CN101575321B CN 101575321 B CN101575321 B CN 101575321B CN 2009100995184 A CN2009100995184 A CN 2009100995184A CN 200910099518 A CN200910099518 A CN 200910099518A CN 101575321 B CN101575321 B CN 101575321B
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trimetazidine
nickel
piperazine
production method
trimethoxybenzaldehyde
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CN101575321A (en
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齐陈泽
姚献东
孙旭东
曾敏峰
沈永淼
肖慧泉
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BEIJING JIALIN PHARMACEUTICAL Co Ltd
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University of Shaoxing
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Abstract

本发明公开了一种曲美他嗪及其盐酸盐的生产方法,属于化工合成技术领域,其特征在于,采用2,3,4-三甲氧基苯甲醛和哌嗪为原料,包括以下步骤:向压力釜中加入溶剂,摩尔比为1∶1~1∶3的2,3,4-三甲氧基苯甲醛与无水哌嗪,占2,3,4-三甲氧基苯甲醛和无水哌嗪质量百分比3~10%的镍型催化剂,通入氢气前先用氮气吹扫,氢压维持在0.7~2.0MPa,反应温度50~95℃,反应时间为4~10小时,将pH值调到3~4,分出有机相,回收溶剂,水相用氯代烃萃洗,将pH值调到12,水相再用芳烃萃取,蒸去芳烃萃取液中的芳烃,即得曲美他嗪。本发明具有生产成本低、收率高、环保性好的优点。The invention discloses a production method of trimetazidine and its hydrochloride, which belongs to the technical field of chemical synthesis, and is characterized in that 2,3,4-trimethoxybenzaldehyde and piperazine are used as raw materials, comprising the following steps : add solvent in autoclave, 2,3,4-trimethoxybenzaldehyde and anhydrous piperazine are 1:1~1:3 in molar ratio, account for 2,3,4-trimethoxybenzaldehyde and anhydrous piperazine The nickel-type catalyst with a mass percentage of water piperazine of 3-10% is purged with nitrogen before introducing hydrogen, the hydrogen pressure is maintained at 0.7-2.0MPa, the reaction temperature is 50-95°C, and the reaction time is 4-10 hours. Adjust the pH value to 3 to 4, separate the organic phase, recover the solvent, wash the water phase with chlorinated hydrocarbons, adjust the pH value to 12, extract the water phase with aromatics, and evaporate the aromatics in the aromatics extract to obtain koji methazine. The invention has the advantages of low production cost, high yield and good environmental protection.

Description

The production method of trimetazidine and hydrochloride thereof
Technical field
The present invention relates to a kind of employing nickel class Preparation of Catalyst anti-anginal drug trimetazidine chemical name is the production method of 1-(2,3,4-trimethoxy benzyl) piperazine (formula 1) and hydrochloride thereof.
Figure G2009100995184D00011
Formula 1
Technical background
Trimetazidine is to begin existing bibliographical information (Fr M805 in 1961; 1961.10.16), (EP 453365 just to research and develop successful a kind of coronary artery expander by French Shi Weiya (Souvie) company by 1991; US 5142053), it can promote the generation of myocardial metabolism and cardiac energy, can reduce myocardial consumption of oxygen simultaneously, thereby improve the equilibrium of supply and demand of myocardium oxygen, also can increase the tolerance to cardiac glycoside.Have effect, can reduce vascular resistance, increase coronary artery and blood flow antiadrenergic drug, norepinephrine and vassopressin.Particularly trimetazidine can increase the sporting trial tolerance of patient with angina pectoris, the myocardial ischemia that delayed motion is brought out, but do not cause Changes of hemodynamics.Can limit quick fluctuation of blood pressure and not cause the heart rate noticeable change, significantly reduce the angina pectoris attacks frequency.
Reported that the method for preparing beautiful his piperazine has following:
1. with 2,3,4-trimethoxy benzyl chloride and 2-piperazine reactive ketone generate 4-(2,3,4-trimethoxy benzyl)-2-piperazine ketone, use LiAlH then 4Be reduced to 2,3,4-trimethoxy benzyl diethylenediamine (being trimetazidine) (FR 2493316)
2. with 1,2, the 3-trimethoxy-benzene is a starting raw material, through 2,3,4-trimethoxy benzyl chloride intermediate and piperazine prepared in reaction (Wang Wenhao, Zhang Xin, Xu Ping, Chinese pharmaceutical chemistry magazine, 2003,13,219-221)
Figure G2009100995184D00022
3. pass through 2,3, the condensation prepared (US3262852 of 4-trimethoxy benzyl chloride and N-formyl piperazine; GB 929252)
Figure G2009100995184D00023
4. pass through with 2,3,4-TMB and piperazine are made the LiAlH of raw material 4Or NaBH 4Amination reduction reaction preparation (CN 1715275)
Figure G2009100995184D00024
5. pass through with 2,3,4-TMB and piperazine are made the LiAlH of raw material 4Or NaBH 4Amination reduction reaction preparation (US 5142053; RU 2234501; EP 453365)
Figure G2009100995184D00031
Preceding four kinds of method product yields are all very low, and production cost is higher, and the 4th kind of method also will be used dangerous bigger LiAlH 4And NaBH 4Reductive agent, and normal at present the 5th route that adopts uses noble metal catalyst mostly, all has some defectives.The application's main purpose is more perfect, practicable production trimetazidine novel method of development.
Summary of the invention
At the problems referred to above of prior art, main purpose of the present invention provides a kind of production method of trimetazidine.
The technical scheme that the present invention takes is as follows, a kind of production method of trimetazidine, adopt 2,3,4-TMB and piperazine are raw material, may further comprise the steps: in autoclave pressure, add solvent, solvent be selected from benzene, toluene, dimethoxy ether, Di Iso Propyl Ether, methyl tertiary butyl ether, ethanol, Virahol etc. any one or a few; Add 2 again, 3, the 4-TMB, Piperazine anhydrous and nickel type catalyzer, what nickel type catalyzer adopted is nickel/diatomite, nickel/aluminum oxide, nickel borides/silica gel, Raney's nickel, nickel formate etc. any one, 2,3,4-TMB and Piperazine anhydrous mol ratio are 1: 1~1: 3, and the catalyzer addition is 2,3,3~10% (weight) of 4-TMB and Piperazine anhydrous total amount, earlier use nitrogen purging before feeding hydrogen, hydrogen pressure maintains 0.7~2.0MPa, reacts temperature required 50~95 ℃, reaction times is 4~10 hours, reaction is to no longer absorbing hydrogen, cooling, release, filter, in filtrate, add water, with hydrochloric acid the pH value is transferred to 3~4, tell organic phase, reclaim solvent, the water hydrochloric ether, as methylene dichloride, chloroform, collections such as ethylene dichloride are washed, with the sodium hydroxide solution pH=12 that neutralizes, water is used aromatic hydrocarbons (benzene more again, toluene) extraction boils off the aromatic hydrocarbons in the aromatic hydrocarbons extraction liquid, promptly get trimetazidine, yield 82~90%.
Secondary objective of the present invention provides a kind of trimetazidine hydrochloride, chemical name is 1-(2,3,4-trimethoxy benzyl) production method of piperazine dihydrochloride (formula 2), with the solution of the above-mentioned trimetazidine that makes in lower alcohol or ether solvents, described solvent can be a methyl alcohol, ethanol, Virahol, ether, the dimethoxy ether, any one of tetrahydrofuran (THF) or two kinds, join in the solution that fills lower alcohols or ether solvent and concentrated hydrochloric acid, stirring reaction 0.5~3 hour, steam and remove partial solvent, be cooled to 0 ℃, filter, filter cake washs with alcoholic solvent, dry, get the trimetazidine hydrochloride, yield 78~92%.
Figure G2009100995184D00041
Formula 2
The beneficial effect of the invention
At first, the present invention has adopted advanced catalytic reduction amination method technology, carries out the amination reduction reaction in the presence of nickel type catalyzer and hydrogen, after making trimetazidine, then be converted into its hydrochloride, adopt production method of the present invention, can make the purpose product yield improve about 40-50%;
Secondly, the present invention has used cheap nickel catalyzator, and product yield is close with the use precious metals palladium catalyst, thereby has reduced production cost;
Simultaneously, the present invention has avoided using dangerous bigger reductive agent LiAlH 4And NaBH 4, strengthened the security of operating process.
Below by specific embodiment the present invention is specifically described, but the present invention is not limited to following example.
Embodiment
The present invention is described further below in conjunction with the embodiment of the invention; be necessary to be pointed out that at this following examples only are used for the present invention is further detailed; can not be interpreted as limiting the scope of the invention, the person skilled in the art in this field can make some nonessential improvement and adjustment to the present invention according to the invention described above content.
Embodiment 1
In autoclave, throw 196 gram (1.0 moles) 2,3, the 4-TMB, 215 gram (2.5 moles) Piperazine anhydrous, 1500 milliliters of dimethoxy ether and 25 gram 5% nickel/diatomite catalyzer are after the nitrogen purging system, fill hydrogen to 1.5MPa, be warming up to 75~85 ℃, stirring reaction 6~8 hours to reactant no longer absorbs hydrogen, cooling, release, filter reaction mixture, in filtrate, add 500 ml waters, the pH value is transferred to 3~4, tell organic phase with the hydrochloric acid of concentration 6M, water is washed 3 times with each ethylene dichloride of 150 milliliters, water neutralizes behind the pH=12 with 460 grams, 50% sodium hydroxide solution again, extracts the combined benzene extraction phase 3 times with each 120 milliliters of benzene, boil off benzene, get trimetazidine 239 grams (~90%).
Embodiment 2
In autoclave, throw 98 gram (0.5 moles) 2,3, the 4-TMB, 86 gram (1.0 moles) Piperazine anhydrous, 500 milliliters of Di Iso Propyl Ethers and 15 gram 8% nickel/aluminium oxide catalysts are after the nitrogen purging system, fill hydrogen to 1.8MPa, be warming up to 85~95 ℃, stirring reaction 8 hours to reactant no longer absorbs hydrogen, cooling, release, product is filtered, in filtrate, add 250 ml waters, the pH value is transferred to 3~4, tell organic phase with the hydrochloric acid of concentration 6M, water is washed 3 times with each ethylene dichloride of 100 milliliters, with 220 grams, the 50% sodium hydroxide solution pH=12 that neutralizes, water extracts the combining methylbenzene extraction phase 3 times with each 80 milliliters of toluene more again, boil off toluene, get trimetazidine 108 grams (81%).
Embodiment 3
In there-necked flask, add 400 milliliters of ethanol, 65 milliliter 35% concentrated hydrochloric acid, under agitation, the drips of solution of 133 gram trimetazidines (0.5 mole) in 280 milliliters of ethanol of embodiment 1 gained is added in the above-mentioned hydrochloric acid soln, after adding, restir 1 hour, normal pressure steam down and remove partial solvent, after overhead product reaches 260 grams, reaction system is cooled to 0 ℃, filters filter cake washing with alcohol, drying, get 155.6 gram trimetazidine dihydrochlorides, yield 92%.

Claims (4)

1.一种曲美他嗪的生产方法,其特征在于,采用2,3,4-三甲氧基苯甲醛和哌嗪为原料,包括以下步骤:向压力釜中加入溶剂,摩尔比为1∶1~1∶3的2,3,4-三甲氧基苯甲醛与无水哌嗪,占2,3,4-三甲氧基苯甲醛和无水哌嗪质量百分比3~10%的镍型催化剂,镍型催化剂选自镍/硅藻土、镍/氧化铝、硼化镍/硅胶、雷尼镍、甲酸镍的任意一种;通入氢气前先用氮气吹扫,氢压维持在0.7~2.0MPa,反应温度50~95℃,反应时间为4~10小时,反应至不再吸收氢,冷却、卸压、过滤,向滤液中加水,将pH值调到3~4,分出有机相,回收溶剂,水相用氯代烃萃洗,将pH值调到12,水相再用芳烃萃取,蒸去芳烃萃取液中的芳烃,即得曲美他嗪。1. a production method of trimetazidine, is characterized in that, adopts 2,3,4-trimethoxybenzaldehyde and piperazine are raw materials, comprise the following steps: add solvent in autoclave, and mol ratio is 1: 1~1:3 2,3,4-trimethoxybenzaldehyde and anhydrous piperazine, nickel-type catalyst accounting for 3~10 mass percent of 2,3,4-trimethoxybenzaldehyde and anhydrous piperazine The nickel-type catalyst is selected from any one of nickel/diatomaceous earth, nickel/alumina, nickel boride/silica gel, Raney nickel, and nickel formate; it is purged with nitrogen before hydrogen gas is introduced, and the hydrogen pressure is maintained at 0.7~ 2.0MPa, reaction temperature 50-95°C, reaction time 4-10 hours, react until hydrogen is no longer absorbed, cool, depressurize, filter, add water to the filtrate, adjust the pH value to 3-4, separate the organic phase , recover the solvent, extract and wash the aqueous phase with chlorinated hydrocarbons, adjust the pH value to 12, extract the aqueous phase with aromatic hydrocarbons, and evaporate the aromatic hydrocarbons in the aromatic hydrocarbon extract to obtain trimetazidine. 2.如权利要求1所述的一种曲美他嗪的生产方法,其特征在于:溶剂选自苯、甲苯、二甲氧基乙醚、二异丙基醚、甲基叔丁基醚、乙醇、异丙醇的任意一种或几种。2. the production method of a kind of trimetazidine as claimed in claim 1 is characterized in that: solvent is selected from benzene, toluene, dimethoxyethyl ether, diisopropyl ether, methyl tertiary butyl ether, ethanol , Any one or more of isopropanol. 3.如权利要求1所述的一种曲美他嗪的生产方法,其特征在于:氯代烃选自二氯甲烷、氯仿、二氯乙烷的任意一种。3. a kind of production method of trimetazidine as claimed in claim 1 is characterized in that: chlorinated hydrocarbon is selected from any one of dichloromethane, chloroform, ethylene dichloride. 4.如权利要求1所述的一种曲美他嗪的生产方法,其特征在于:芳烃选自苯、甲苯的一种。4. a kind of production method of trimetazidine as claimed in claim 1 is characterized in that: aromatic hydrocarbon is selected from the one of benzene, toluene.
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Publication number Priority date Publication date Assignee Title
CN102140084A (en) * 2010-02-03 2011-08-03 辽宁本源制药有限公司 A kind of production method of trimetazidine and its hydrochloride
CN102010386B (en) * 2010-11-10 2012-07-11 武汉武药科技有限公司 Method for preparing trimetazidine hydrochloride
CN102850296B (en) * 2012-09-29 2015-01-07 瑞阳制药有限公司 Preparation method of trimetazidine
CN102993122B (en) * 2012-12-24 2015-03-04 武汉武药制药有限公司 Novel synthesis path of trimetazidine hydrochloride
CN103554057B (en) * 2013-11-13 2016-04-20 武汉武药科技有限公司 Trimetazidine derivative and preparation method thereof
CN110713471B (en) * 2018-07-13 2022-05-06 北京福元医药股份有限公司沧州分公司 Synthetic method of trimetazidine hydrochloride
CN116041280B (en) * 2022-12-05 2024-07-05 三峡大学 Preparation method of trimetazidine hydrochloride
CN118420566B (en) * 2024-04-26 2025-03-11 海南锦麟医药科技有限公司 Preparation method of high-purity trimetazidine hydrochloride

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1302958A (en) * 1961-03-21 1962-09-07 Science Union & Cie Preparations of trialkoxylated derivatives of 1-benzyl piperazine
US5142053A (en) * 1990-04-20 1992-08-25 Adir Et Compagnie Process for the preparation of 1-(2,3,4-trimethoxybenzyl)piperazine by reductive animation
CN1715275A (en) * 2004-06-29 2006-01-04 北京德众万全药物技术开发有限公司 Simple process for preparing trimetazidine and its medicinal salts

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1302958A (en) * 1961-03-21 1962-09-07 Science Union & Cie Preparations of trialkoxylated derivatives of 1-benzyl piperazine
US5142053A (en) * 1990-04-20 1992-08-25 Adir Et Compagnie Process for the preparation of 1-(2,3,4-trimethoxybenzyl)piperazine by reductive animation
CN1715275A (en) * 2004-06-29 2006-01-04 北京德众万全药物技术开发有限公司 Simple process for preparing trimetazidine and its medicinal salts

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
王文浩等.曲美他嗪合成方法的改进.《中国药物化学杂志》.2003,第13卷(第4期),119-221. *

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Assignee: Beijing Jialin Pharmaceutical Co., Ltd.

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Denomination of invention: Trimetazidine and production method for hydrochloride of trimetazidine

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